Optimization for large scale process based on evolutionary algorithms: Genetic algorithms
This work has as objective the development of an optimization methodology, using Genetic Algorithms (GAs), as evolutionary procedure coupled with the concepts of evolutionary. As case study a large scale multiphase catalytic reactor is considered. The reactor is tubular in shape and is built-up with...
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| Published in | Chemical engineering journal (Lausanne, Switzerland : 1996) Vol. 132; no. 1; pp. 1 - 8 |
|---|---|
| Main Authors | , , , , |
| Format | Journal Article |
| Language | English |
| Published |
Amsterdam
Elsevier B.V
01.08.2007
Elsevier |
| Subjects | |
| Online Access | Get full text |
| ISSN | 1385-8947 1873-3212 |
| DOI | 10.1016/j.cej.2006.12.032 |
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| Abstract | This work has as objective the development of an optimization methodology, using Genetic Algorithms (GAs), as evolutionary procedure coupled with the concepts of evolutionary. As case study a large scale multiphase catalytic reactor is considered. The reactor is tubular in shape and is built-up with concentric tubes using the same concept of the auto-thermal reactors, with coolant fluid flow in the external annular. The mathematical equations of the deterministic model are based on conservation principles (mass, energy and momentum) for the reactants and for the coolant fluid and validated with real operational data. The model represents the steady-state with the plug-flow assumption which is quite reasonable due to the large flow rates usually found in industrial reactors. The desired product is a specific cyclical alcohol (CA), and the minimization of the by-products is required for economical and environmental reasons. For that it is necessary to optimize some important operational parameters. This problem is of difficult solution since the reactor is a large scale system with complex behavior and conventional optimization tools as Successive Quadratic Programming tends to fail in such situation since local minima may be achieved.
In this work is shown that the Genetic Algorithms technique can be useful to CA production maximization, obtaining good results with operational improvements (reduction in the catalyst rate, as well as in the undesired product rate—cycloalkane (C)). The GA parameters used for the process optimization are population size, crossover types with variation of crossover rates. The used coding was the binary form.
The results are quite good, showing high performance in the CA productivity (considerable increase CA production) with changes in the operational parameters analyzed and showing that this optimization procedure is very robust and efficient. The results point out that this technique is very promising to deal with large scale system with complex behavior due to non-linearity and variable interactions. |
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| AbstractList | This work has as objective the development of an optimization methodology, using Genetic Algorithms (GAs), as evolutionary procedure coupled with the concepts of evolutionary. As case study a large scale multiphase catalytic reactor is considered. The reactor is tubular in shape and is built-up with concentric tubes using the same concept of the auto-thermal reactors, with coolant fluid flow in the external annular. The mathematical equations of the deterministic model are based on conservation principles (mass, energy and momentum) for the reactants and for the coolant fluid and validated with real operational data. The model represents the steady-state with the plug-flow assumption which is quite reasonable due to the large flow rates usually found in industrial reactors. The desired product is a specific cyclical alcohol (CA), and the minimization of the by-products is required for economical and environmental reasons. For that it is necessary to optimize some important operational parameters. This problem is of difficult solution since the reactor is a large scale system with complex behavior and conventional optimization tools as Successive Quadratic Programming tends to fail in such situation since local minima may be achieved.
In this work is shown that the Genetic Algorithms technique can be useful to CA production maximization, obtaining good results with operational improvements (reduction in the catalyst rate, as well as in the undesired product rate—cycloalkane (C)). The GA parameters used for the process optimization are population size, crossover types with variation of crossover rates. The used coding was the binary form.
The results are quite good, showing high performance in the CA productivity (considerable increase CA production) with changes in the operational parameters analyzed and showing that this optimization procedure is very robust and efficient. The results point out that this technique is very promising to deal with large scale system with complex behavior due to non-linearity and variable interactions. This work has as objective the development of an optimization methodology, using Genetic Algorithms (GAs), as evolutionary procedure coupled with the concepts of evolutionary. As case study a large scale multiphase catalytic reactor is considered. The reactor is tubular in shape and is built-up with concentric tubes using the same concept of the auto-thermal reactors, with coolant fluid flow in the external annular. The mathematical equations of the deterministic model are based on conservation principles (mass, energy and momentum) for the reactants and for the coolant fluid and validated with real operational data. The model represents the steady-state with the plug-flow assumption which is quite reasonable due to the large flow rates usually found in industrial reactors. The desired product is a specific cyclical alcohol (CA), and the minimization of the by-products is required for economical and environmental reasons. For that it is necessary to optimize some important operational parameters. This problem is of difficult solution since the reactor is a large scale system with complex behavior and conventional optimization tools as Successive Quadratic Programming tends to fail in such situation since local minima may be achieved. In this work is shown that the Genetic Algorithms technique can be useful to CA production maximization, obtaining good results with operational improvements (reduction in the catalyst rate, as well as in the undesired product rate--cycloalkane (C)). The GA parameters used for the process optimization are population size, crossover types with variation of crossover rates. The used coding was the binary form. The results are quite good, showing high performance in the CA productivity (considerable increase CA production) with changes in the operational parameters analyzed and showing that this optimization procedure is very robust and efficient. The results point out that this technique is very promising to deal with large scale system with complex behavior due to non-linearity and variable interactions. |
| Author | Wolf Maciel, M.R. Maia, J.P. Filho, R. Maciel Morais, E.R. Victorino, I.R.S. |
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| Keywords | Global optimization C Not Opt CEX GAs Three phase catalytic reactor GA CA BA Genetic algorithms Coolant Reaction product Catalytic reactor Momentum Quadratic programming Modeling Steady state Optimization Plug flow Genetic algorithm Deterministic model Morphology Production Catalyst Mathematical programming |
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| References | I.R.S. Victorino, Optimization of an industrial reactor of cyclic alcohol production using genetic algorithms, Ph.D. Thesis, School of Chemical Engineering, Unicamp, São Paulo, Brazil, 2005 (in Portuguese). Deb (bib9) 1998 Goldberg (bib5) 1989 P.L. Santana, Mathematical modeling for three phase reactor: deterministic, neural and hybrid models, Ph.D. Thesis, School of Chemical Engineering, Unicamp, São Paulo, Brazil, 1995 (in Portuguese). Froment, Bischoff (bib6) 1990 Carroll (bib8) 1996; 34 Bäck, Fogel, Michalewicz (bib10) 2000 Holland (bib4) 1992 Coussemant, Jungers (bib7) 1950; 59 Vasco De Toledo, Santana, Wolf-Maaciel, Maciel Filho (bib1) 2001; 56 10.1016/j.cej.2006.12.032_bib3 Vasco De Toledo (10.1016/j.cej.2006.12.032_bib1) 2001; 56 10.1016/j.cej.2006.12.032_bib2 Froment (10.1016/j.cej.2006.12.032_bib6) 1990 Deb (10.1016/j.cej.2006.12.032_bib9) 1998 Holland (10.1016/j.cej.2006.12.032_bib4) 1992 Goldberg (10.1016/j.cej.2006.12.032_bib5) 1989 Carroll (10.1016/j.cej.2006.12.032_bib8) 1996; 34 Coussemant (10.1016/j.cej.2006.12.032_bib7) 1950; 59 Bäck (10.1016/j.cej.2006.12.032_bib10) 2000 |
| References_xml | – volume: 56 start-page: 6055 year: 2001 end-page: 6061 ident: bib1 article-title: Dynamic modeling of a three-phase catalytic slurry reactor publication-title: Chem. Eng. Sci. – year: 1992 ident: bib4 article-title: Adaptation in Natural and Artificial Systems – volume: 59 start-page: 295 year: 1950 end-page: 326 ident: bib7 article-title: La Cinétique de ĹHydrogénation Catalytique des Phénols publication-title: Bull. Soc. Chim. Bel. – reference: I.R.S. Victorino, Optimization of an industrial reactor of cyclic alcohol production using genetic algorithms, Ph.D. Thesis, School of Chemical Engineering, Unicamp, São Paulo, Brazil, 2005 (in Portuguese). – start-page: 58 year: 1998 end-page: 87 ident: bib9 article-title: Genetic algorithms in search and optimization: the technique and applications publication-title: Proceedings of International Workshop on Soft Computing and Intelligent Systems – year: 2000 ident: bib10 article-title: Evolutionary Computation 1: Basic Algorithms and Operators – volume: 34 year: 1996 ident: bib8 article-title: Chemical laser modeling with genetic algorithms publication-title: AIAA J. – year: 1989 ident: bib5 article-title: Genetic Algorithms in Search, Optimization, and Machine Learning – reference: P.L. Santana, Mathematical modeling for three phase reactor: deterministic, neural and hybrid models, Ph.D. Thesis, School of Chemical Engineering, Unicamp, São Paulo, Brazil, 1995 (in Portuguese). – year: 1990 ident: bib6 article-title: Chemical Reactor Analysis and Design – year: 1990 ident: 10.1016/j.cej.2006.12.032_bib6 – start-page: 58 year: 1998 ident: 10.1016/j.cej.2006.12.032_bib9 article-title: Genetic algorithms in search and optimization: the technique and applications – year: 1992 ident: 10.1016/j.cej.2006.12.032_bib4 – year: 1989 ident: 10.1016/j.cej.2006.12.032_bib5 – year: 2000 ident: 10.1016/j.cej.2006.12.032_bib10 – ident: 10.1016/j.cej.2006.12.032_bib3 – ident: 10.1016/j.cej.2006.12.032_bib2 – volume: 56 start-page: 6055 year: 2001 ident: 10.1016/j.cej.2006.12.032_bib1 article-title: Dynamic modeling of a three-phase catalytic slurry reactor publication-title: Chem. Eng. Sci. doi: 10.1016/S0009-2509(01)00260-3 – volume: 34 issue: February (2) year: 1996 ident: 10.1016/j.cej.2006.12.032_bib8 article-title: Chemical laser modeling with genetic algorithms publication-title: AIAA J. – volume: 59 start-page: 295 year: 1950 ident: 10.1016/j.cej.2006.12.032_bib7 article-title: La Cinétique de ĹHydrogénation Catalytique des Phénols publication-title: Bull. Soc. Chim. Bel. |
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| SubjectTerms | Applications of mathematics to chemical engineering. Modeling. Simulation. Optimization Applied sciences Catalysis Catalytic reactions Chemical engineering Chemistry Exact sciences and technology General and physical chemistry Genetic algorithms Global optimization Reactors Theory of reactions, general kinetics. Catalysis. Nomenclature, chemical documentation, computer chemistry Three phase catalytic reactor |
| Title | Optimization for large scale process based on evolutionary algorithms: Genetic algorithms |
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